CN205307876U - Coalescence -separation jar - Google Patents
Coalescence -separation jar Download PDFInfo
- Publication number
- CN205307876U CN205307876U CN201521007377.6U CN201521007377U CN205307876U CN 205307876 U CN205307876 U CN 205307876U CN 201521007377 U CN201521007377 U CN 201521007377U CN 205307876 U CN205307876 U CN 205307876U
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- China
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- filter core
- oil
- water
- tank body
- level probe
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Abstract
The utility model relates to a coalescence -separation jar, including a jar body, coalescence filter core and separation filter core, the coalescence filter core with the separation filter core all sets up the inside of the jar body, oil inlet and oil -out have been seted up on the jar body, the coalescence filter core with the oil inlet is linked together, the separation filter core with the oil -out is linked together. The utility model provides a coalescence -separation jar, coalescence -separation jar uses coalescence filter core and separation filter core to separate water oil simultaneously, has optimized the filter core mounting means, convenient with the help of gravity install and change the filter core, area is less simultaneously.
Description
Technical field
The utility model belongs to the separating of oil apparatus field of water, is specifically related to a kind of coarse separation tank.
Background technology
Coarse separation tank is a kind of separating of oil equipment of water, being widely used containing in oil treatment in departments such as oil field, refinery, chemical industry, machinery or light industrys. Along with the Deep mining of oil, the maximization development of chemical enterprise and the strict demand to environment protection, oily water separation technique is paid attention to day by day.
Contriver is in the process using traditional coarse separation tank, it has been found that have following problem, as: change the problem that filter core is inconvenient, floor space is big.
Practical novel content
In order to solve the problems referred to above that prior art exists, the utility model provides a kind of coarse separation tank, described coarse separation tank uses Coalescence filter core simultaneously, and water oil is separated by filter core with being separated, in addition, described coarse separation tank adopts the mode vertically arranged, optimize filter core and install mode, convenient installed by filter core by gravity and change, floor space is less simultaneously.
The technical scheme that the utility model adopts is: a kind of coarse separation tank, comprise tank body, Coalescence filter core and it is separated filter core, described Coalescence filter core is separated, with described, the inside that filter core is all arranged on described tank body, having offered oil-in and oil outlet on described tank body, described Coalescence filter core is connected with described oil-in; Described separation filter core is connected with described oil outlet.
Have in other words, in use, oil containing moisture enters tank body by described oil-in, in described tank body successively through Coalescence filter core be separated filter core, oil containing moisture is carried out initial gross separation by Coalescence filter core, separation filter core carry out secondary separation, carry out water separating of oil after, almost moisture free oil is discharged from described oil outlet, is deposited on described tank base after hydrogenesis.
In order to strengthen processing power and the separating effect of described coarse separation tank further, preferred technical scheme is, the number of described Coalescence filter core is multiple, and multiple described Coalescence filter core is arranged side by side in described tank body, and multiple described Coalescence filter core adopts form in parallel to be connected with described oil-in;The number of described separation filter core is multiple, and multiple described separation filter core is arranged side by side in described tank body, and multiple described separation filter core adopts form in parallel to be connected with described oil outlet.
Multiple Coalescence filter core, with being separated filter core and be and be arranged in parallel, increases the processing power of described coarse separation tank, and in addition, under same processing power, the setting of multiple filter core can use the longer time, simplifies operation.
Be deposited on the water of described tank base to automatically discharge, it is preferable that technical scheme be that the bottom of described tank body is provided with water outlet, is provided with valve in described water outlet; The inwall of described tank body is also provided with oil level probe and water-level probe, and described water-level probe is arranged on described Coalescence filter core and the lower section being separated filter core, and described oil level probe is arranged on the lower section of described water-level probe; Described oil level is popped one's head in and water-level probe all links with described valve and controls the keying of described valve.
Concrete control mode is: because the density of water is bigger than oil, so water is in the lower section of oil; When described water-level probe detects water, Open valve, water flows out from described water outlet, and when described oil level probe detects oil, valve-off, prevents oil from flowing out from described water outlet. By the linkage of above-mentioned probe and described valve, can ensure that water oil interface is between described oil level probe and water-level probe always. Above-mentioned detection and control mode, all belong to prior art, and those skilled in the art all can obtain easily, just repeats no more at this.
In order to reduce the turbulent flow of described tank base, it is preferable that technical scheme be also comprise dividing plate, described diaphragm rings paste described tank body inwall arrange, described dividing plate is arranged between described water-level probe and described Coalescence filter core; Described dividing plate is offered the through hole on vertical direction. Described dividing plate greatly reduces the turbulent flow of tank base, makes to have between water oil separation surface clearly, is convenient to the detection of described oil level probe and water-level probe.
As a kind of concrete set-up mode, the number of described dividing plate is two, is respectively dividing plate and lower clapboard, and described oil-in is arranged between described upper dividing plate and lower clapboard. Described upper dividing plate is identical with lower clapboard shape, and the through hole being opened on two described dividing plates respectively overlaps in the projection of vertical direction. Being arranged on by oil-in between described upper dividing plate and lower clapboard, described upper dividing plate and lower clapboard can also play the effect that the oil guided containing moisture enters described Coalescence filter core, further increase the processing power of described coarse separation tank.
For the ease of maintenance and change filter core, it is preferable that technical scheme be that described coarse separation tank also comprises cover plate, described cover plate is removably installed in the top of described tank body by flange. Open the mode detachably connected, it is convenient to the maintenance in later stage.
It should be noted that, be reduce floor space, in the utility model, described coarse separation tank vertically places, from open top and the mode of cover plate is set, convenient by gravity filter core installed and change.
The beneficial effects of the utility model are:
1, the utility model provides a kind of coarse separation tank, described coarse separation tank uses Coalescence filter core simultaneously, and water oil is separated by filter core with being separated, in addition, described coarse separation tank adopts the mode vertically arranged, optimize filter core and install mode, convenient installed by filter core by gravity and change, floor space is less simultaneously.
2, in the utility model, by the linkage of above-mentioned probe and described valve, can ensure that water oil interface is between described oil level probe and water-level probe always, it is achieved that automatically control.
3, arranging dividing plate in the tank body in the utility model, described dividing plate greatly reduces the turbulent flow of tank base, makes to have between water oil separation surface clearly, is convenient to the detection of described oil level probe and water-level probe.
Accompanying drawing explanation
Fig. 1 is sectional view of the present utility model;
Fig. 2 is sectional view of the present utility model.
In figure: 1, tank body; 2, Coalescence filter core; 3, it is separated filter core; 4, oil-in; 5, oil outlet; 6, water outlet; 7, oil level probe; 8, water-level probe; 9, upper dividing plate; 10, lower clapboard; 11, cover plate; 12, flange.
Embodiment
As shown in Figure 1, the utility model provides a kind of coarse separation tank, comprise tank body 1, Coalescence filter core 2 and it is separated filter core 3, described Coalescence filter core 2 is separated, with described, the inside that filter core 3 is all arranged on described tank body 1, having offered oil-in 4 and oil outlet 5 on described tank body 1, described Coalescence filter core 2 is connected with described oil-in 4; Described separation filter core 3 is connected with described oil outlet 5.
In use, oil containing moisture enters tank body 1 by described oil-in 4, in described tank body 1 successively through Coalescence filter core 2 be separated filter core 3, oil containing moisture is carried out initial gross separation by Coalescence filter core 2, separation filter core 3 carries out secondary separation, carry out water separating of oil after, almost moisture free oil is discharged from described oil outlet 5, is deposited on bottom described tank body 1 after hydrogenesis.
In order to strengthen processing power and the separating effect of described coarse separation tank further, contriver has following setting, the number of described Coalescence filter core 2 is multiple, multiple described Coalescence filter core 2 is arranged side by side in described tank body 1, and multiple described Coalescence filter core 2 adopts form in parallel to be connected with described oil-in 4; The number of described separation filter core 3 is multiple, and multiple described separation filter core 3 is arranged side by side in described tank body 1, and multiple described separation filter core 3 adopts form in parallel to be connected with described oil outlet 5. Multiple Coalescence filter core 2, with being separated filter core 3 and be and be arranged in parallel, increases the processing power of described coarse separation tank, and in addition, under same processing power, the setting of multiple filter core can use the longer time, simplifies operation.
It should be noted that, described Coalescence filter core 2 can be nonsynchronous with the selection being separated filter core 3 number, that is, can be multiple described Coalescence filter core 2 and an array configuration being separated filter core 3, can also be a described Coalescence filter core 2 and multiple array configuration being separated filter core 3, such as in the present embodiment, it is exactly adopt three Coalescence filter cores 2 and an array configuration being separated filter core 3.
As described in Figure 2, in order to automatically discharge the water being deposited on bottom described tank body 1, contriver has following setting, and the bottom of described tank body 1 is provided with water outlet 6, is provided with valve in described water outlet 6; The inwall of described tank body 1 is also provided with oil level probe 7 and water-level probe 8, and described water-level probe 8 is arranged on described Coalescence filter core 2 and the lower section being separated filter core 3, and described oil level probe 7 is arranged on the lower section of described water-level probe 8; Described oil level probe 7 and water-level probe 8 all link with described valve and control the keying of described valve.
Concrete control mode is: because the density of water is bigger than oil, so water is in the lower section of oil; When described water-level probe 8 detects water, Open valve, water flows out from described water outlet 6, and when described oil level probe 7 detects oil, valve-off, prevents oil from flowing out from described water outlet 6.By the linkage of above-mentioned probe and described valve, can ensure that water oil interface is between described oil level probe 7 and water-level probe 8 always.
As described in Figure 2, in order to reduce the turbulent flow bottom described tank body 1, contriver has following setting, also comprises dividing plate, and the inwall that described diaphragm rings pastes described tank body 1 is arranged, and described dividing plate is arranged between described water-level probe 8 and described Coalescence filter core 2; Described dividing plate is offered the through hole on vertical direction. Described dividing plate greatly reduces the turbulent flow bottom tank body 1, makes to have between water oil separation surface clearly, is convenient to the detection of described oil level probe 7 and water-level probe 8.
A kind of concrete set-up mode is that the number of described dividing plate is two, is respectively dividing plate 9 and lower clapboard 10, and described oil-in 4 is arranged between described upper dividing plate 9 and lower clapboard 10. Described upper dividing plate 9 is identical with lower clapboard 10 shape, and the through hole being opened in two described dividing plates respectively overlaps in the projection of vertical direction. Oil-in 4 is arranged between described upper dividing plate 9 and lower clapboard 10, described upper dividing plate 9 and lower clapboard 10 can also play the effect that the oil guided containing moisture enters described Coalescence filter core 2, described oil-in 4 is directly connected with described Coalescence filter core 2, further increases the processing power of described coarse separation tank.
Described coarse separation tank also comprises cover plate 11, and described cover plate 11 is removably installed in the top of described tank body 1 by flange 12. The mode removably connected, is convenient to the maintenance in later stage and changes filter core.
The utility model is not limited to above-mentioned preferred forms; anyone can draw the product of other various forms under enlightenment of the present utility model; no matter but in its shape or structure, do any change; every have the technical scheme identical or close with the application, all drops within protection domain of the present utility model.
Claims (8)
1. a coarse separation tank, it is characterized in that, comprise tank body, Coalescence filter core and be separated filter core, described Coalescence filter core is separated, with described, the inside that filter core is all arranged on described tank body, having offered oil-in and oil outlet on described tank body, described Coalescence filter core is connected with described oil-in; Described separation filter core is connected with described oil outlet.
2. coarse separation tank according to claim 1, it is characterised in that, the number of described Coalescence filter core is multiple, and multiple described Coalescence filter core is arranged side by side in described tank body, and multiple described Coalescence filter core adopts form in parallel to be connected with described oil-in.
3. coarse separation tank according to claim 1, it is characterised in that, the number of described separation filter core is multiple, and multiple described separation filter core is arranged side by side in described tank body, and multiple described separation filter core adopts form in parallel to be connected with described oil outlet.
4. according to the arbitrary described coarse separation tank of claim 1-3, it is characterised in that, the bottom of described tank body is provided with water outlet, is provided with valve in described water outlet; The inwall of described tank body is also provided with oil level probe and water-level probe, and described water-level probe is arranged on described Coalescence filter core and the lower section being separated filter core, and described oil level probe is arranged on the lower section of described water-level probe; Described oil level probe and water-level probe all link with described valve, and control the keying of described valve.
5. coarse separation tank according to claim 4, it is characterised in that, also comprise dividing plate, the inwall that described diaphragm rings pastes described tank body is arranged, and described dividing plate is arranged between described water-level probe and described Coalescence filter core;Described dividing plate is offered the through hole on vertical direction.
6. coarse separation tank according to claim 5, it is characterised in that, the number of described dividing plate is two, is respectively dividing plate and lower clapboard, and described oil-in is arranged between described upper dividing plate and lower clapboard.
7. coarse separation tank according to claim 6, it is characterised in that, described upper dividing plate is identical with lower clapboard shape, and the through hole being opened on two described dividing plates respectively overlaps in the projection of vertical direction.
8. coarse separation tank according to claim 4, it is characterised in that, also comprise cover plate, described cover plate is removably installed in the top of described tank body by flange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521007377.6U CN205307876U (en) | 2015-12-03 | 2015-12-03 | Coalescence -separation jar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521007377.6U CN205307876U (en) | 2015-12-03 | 2015-12-03 | Coalescence -separation jar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205307876U true CN205307876U (en) | 2016-06-15 |
Family
ID=56315941
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521007377.6U Expired - Fee Related CN205307876U (en) | 2015-12-03 | 2015-12-03 | Coalescence -separation jar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205307876U (en) |
-
2015
- 2015-12-03 CN CN201521007377.6U patent/CN205307876U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160615 Termination date: 20181203 |